Polypropylene to transportation fuel grade hydrocarbons over γ-alumina catalyst

Sathyapal R. Churipard , Adrian Alejandro Rodriguez Pinos , Sundaramurthy Vedachalam , Maliheh Heravi , Ajay K. Dalai , Saumitra Saxena , Bassam Dally
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Abstract

Catalytic upgrading of plastics to valuable fuels and chemicals is an attractive route to valorize waste plastics. Herein, catalytic pyrolysis of polypropylene was performed over γ-Al2O3 as a heterogeneous catalyst to produce fuel-grade hydrocarbons. The use of an inexpensive γ-Al2O3 catalyst and mild reaction conditions led to high liquid yield selectively in gasoline-range hydrocarbons which stands out from most of the work reported in the literature for polypropylene pyrolysis. The reaction conditions of pyrolysis were optimized by the Box-Behnken Design approach utilizing the response surface methodology. The highest liquid yield of 88.1 wt.% was obtained at 470 °C temperature, with 2 wt.% of catalysts and 5 h reaction time. The amount of solid carbon was insignificant (0.7 wt.%) and the gas yield was 11.2 wt.%. The γ-Al2O3 showed high efficiency and stability for converting polypropylene to liquid fuels. The catalyst was highly stable, reusable, and showed similar catalytic activity for 3 recycles. These features and the highly selective conversion of PP to gasoline range fuels are crucial for large-scale applications. The GC–MS analysis revealed that the liquid fuel produced mostly contained C8 to C15 hydrocarbons encompassing mostly gasoline and a small fraction of diesel fuel and higher hydrocarbons. The GC–MS data was also supported by SimDist analysis, which exhibited the boiling point ranging from 100 °C to 260 °C for the liquid fuel product. The reaction temperature and time had a significant impact on the liquid yield. The higher temperature favored the formation of the gaseous product of C1-C3 hydrocarbons. The NMR analysis showed that the liquid products mostly contained the highest amount of paraffins followed by olefins and a small fraction of aromatics. The presence of mild acidity in the γ-Al2O3 catalyst and optimum reaction condition provides favorable conditions to produce the highest yield of transportation fuel grade hydrocarbons without over-cracking into gases.

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在γ-氧化铝催化剂上将聚丙烯转化为运输燃料级碳氢化合物
将塑料催化升级为有价值的燃料和化学品是实现废塑料价值化的一条极具吸引力的途径。在本文中,以γ-Al2O3 作为异相催化剂对聚丙烯进行了催化热解,以生产燃料级碳氢化合物。使用廉价的 γ-Al2O3 催化剂和温和的反应条件,可选择性地获得高产液量的汽油级碳氢化合物,这与文献中报道的大多数聚丙烯热解研究成果不同。利用响应面方法,采用盒-贝肯设计法对热解反应条件进行了优化。在温度为 470 ℃、催化剂用量为 2 wt.%、反应时间为 5 小时的条件下,液体产率最高,达到 88.1 wt.%。固体碳的数量很少(0.7 wt.%),气体产量为 11.2 wt.%。在将聚丙烯转化为液体燃料的过程中,γ-Al2O3 表现出了高效性和稳定性。该催化剂高度稳定,可重复使用,并在 3 次循环中显示出相似的催化活性。这些特点以及聚丙烯向汽油系列燃料的高选择性转化对于大规模应用至关重要。气相色谱-质谱(GC-MS)分析表明,生产的液体燃料主要含有 C8 至 C15 碳氢化合物,其中大部分是汽油,小部分是柴油和更高的碳氢化合物。SimDist 分析也支持 GC-MS 数据,该分析表明液体燃料产品的沸点范围为 100 °C 至 260 °C。反应温度和时间对液体产率有显著影响。较高的温度有利于 C1-C3 碳氢化合物气态产物的形成。核磁共振分析表明,液态产物中石蜡含量最高,其次是烯烃,还有一小部分芳烃。γ-Al2O3催化剂中的弱酸性和最佳反应条件为生产最高产量的运输燃料级碳氢化合物提供了有利条件,而且不会过度裂解为气体。
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